SU144157A1 - Method for distilling off hydrogen chloride from hydrochloric acid - Google Patents

Method for distilling off hydrogen chloride from hydrochloric acid

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Publication number
SU144157A1
SU144157A1 SU691513A SU691513A SU144157A1 SU 144157 A1 SU144157 A1 SU 144157A1 SU 691513 A SU691513 A SU 691513A SU 691513 A SU691513 A SU 691513A SU 144157 A1 SU144157 A1 SU 144157A1
Authority
SU
USSR - Soviet Union
Prior art keywords
hydrochloric acid
hydrogen chloride
distilling
reflux
reflux condenser
Prior art date
Application number
SU691513A
Other languages
Russian (ru)
Inventor
Э.Р. Берлин
О.З. Брагилевский
Т.Д. Гужновская
Т.Д. Гужновска
С.С. Мильруд
А.Л. Энглин
Original Assignee
Э.Р. Берлин
О.З. Брагилевский
Т.Д. Гужновска
С.С. Мильруд
А.Л. Энглин
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Э.Р. Берлин, О.З. Брагилевский, Т.Д. Гужновска, С.С. Мильруд, А.Л. Энглин filed Critical Э.Р. Берлин
Priority to SU691513A priority Critical patent/SU144157A1/en
Application granted granted Critical
Publication of SU144157A1 publication Critical patent/SU144157A1/en

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Description

По известным способам отгонка хлористого водорода из ооллмой кислоты осуществл етс  либо по принципу простой отгочки, либо гутем применени  дефлегматора дл  образовани  флегмы, которую затем возвращают в ректификационную колонну.According to known methods, the removal of hydrogen chloride from oolmoic acid is carried out either by the principle of simple otgochki or by using a reflux condenser to form a phlegm, which is then returned to the distillation column.

Последний способ, как и первый, не дает надлежащего эффекта, так как образующа с  флегма составл ет ограниченное количество примерно 20% от веса выдел емого хлористого водорода. К тому же малый объем флегмы требует тарельчатой конструкции укрепл ю хей части колонны и обуславливает низкий коэффициент теплопередачи в теплообменнике-дефлегматоре.The latter method, like the first, does not give the proper effect, since the reflux produced is a limited amount of about 20% by weight of the emitted hydrogen chloride. In addition, a small amount of reflux requires a plate-like structure that strengthens the core of the column and causes a low heat transfer coefficient in the heat exchanger-dephlegmator.

Предлагаемый способ лишен указанных недостатков и состоит в том, что роль флегмоной жидкости играет часть исходной сол ной кислот, специально задаваемой в дефлегматор-абсорбер.The proposed method is devoid of the indicated disadvantages and consists in the fact that the role of cellulitis fluid is played by a part of the initial hydrochloric acid, which is specially specified in the reflux condenser-absorber.

Исходна  сол на  кислота насыщаетс  в дефлегматоре-абсорбере хлористым водородом и на выходе из него имеет тот состав, что и естественна  флегмова  жидкость. При флегмовом числе 1,2 (за счет искусственной флегмы, близкой к 1) достигаетс  наиболее выгодное использование расходуемого холода и тепла, а также теплообменной i:oверхности .The initial hydrochloric acid is saturated in the reflux condenser with hydrogen chloride and at the outlet of it has the same composition as the natural reflux liquid. With a reflux ratio of 1.2 (due to artificial reflux close to 1), the most advantageous use of the consumed cold and heat, as well as heat exchange i: o the top, is achieved.

Отличительна  особенность иредлагаемого способа состоит в том, что процесс отгонки ведут с применение.м искусственной флегмы, которую создают укреплением части исходной сол ной кислоты в дефлегматоре-абсорбере .A distinctive feature of the proposed method is that the distillation process is carried out with the use of artificial phlegm, which is created by strengthening part of the initial hydrochloric acid in the reflux condenser-absorber.

Пример. Осуществление процесса по сн етс  схс.ой. Псходна  32%-на  сол на  кислота раздел етс  на 2 потока: поток а- 310 кг/час; поток б-50 кг/час. Пот .ж а подогреваетс  в кип тильнике от 65 до 80° и далее поступает на тарелку питани  ректификационной колонExample. The implementation of the process is explained in cc. The initial 32% hydrochloric acid is divided into 2 streams: a stream a - 310 kg / h; flow b-50 kg / hour. The pot is heated in a boiler from 65 to 80 ° and then fed to the food plate of the distillation column.

SU691513A 1960-12-30 1960-12-30 Method for distilling off hydrogen chloride from hydrochloric acid SU144157A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU691513A SU144157A1 (en) 1960-12-30 1960-12-30 Method for distilling off hydrogen chloride from hydrochloric acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU691513A SU144157A1 (en) 1960-12-30 1960-12-30 Method for distilling off hydrogen chloride from hydrochloric acid

Publications (1)

Publication Number Publication Date
SU144157A1 true SU144157A1 (en) 1961-11-30

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Family Applications (1)

Application Number Title Priority Date Filing Date
SU691513A SU144157A1 (en) 1960-12-30 1960-12-30 Method for distilling off hydrogen chloride from hydrochloric acid

Country Status (1)

Country Link
SU (1) SU144157A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1052732C (en) * 1990-10-26 2000-05-24 辽宁省肿瘤研究所 Natural anti-cancer leukonuclein made from animal spleens

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1052732C (en) * 1990-10-26 2000-05-24 辽宁省肿瘤研究所 Natural anti-cancer leukonuclein made from animal spleens

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